chapter 7. polymer solutions 7.1. criteria for polymers solubility … · 2020. 3. 22. ·...

Ariadne L Juwono

Departemen Fisika FMIPA UISemester I 2006/2007

Chapter 7. Polymer solutions

7.1. Criteria for polymers solubility

7.2. Conformations of dissolved polymer

chains

7.3. Thermodynamics of polymer solutions

7.4. Phase equilibrium in polymer solutions

7.5. Fractionation of polymers by solubility

Ariadne L. Juwono


7.1. Criteria of polymer solubility

The solution processThe polymer dissolving occurs very slow and consists in 2 steps:1. Solvent molecules slowly diffuse into the polymer

a swolen gel. This process is very slow because of crosslinking, crytallinity, orstrong hydrogen bonding.

2. The gel gradually disintegrates into a true solution.Agitation can speed up this process.

For very high molecular weight, the solution process takes days or weeks.

Ariadne L. Juwono


Polymer texture and solubilitySolubility relations in polymer systems are complex, because of•The size differences between polymer and solvent molecules,•The viscosity of the system,•The effects of the texture•The molecular weight of the polymer.

Solubility depends on the nature of the solvent, the temperatureof the solution, the topology of the polymer, and the crystallinity.

Cross-linked polymers do not dissolve, but only swell with the solventwhen an interaction between the polymer and the solvent occurs.

Examples:•Light cross-linked rubbers swell,•Unvulcanized materials would dissolve,•Hard rubbers and thermosetting materials may not swell in any solvent.

Ariadne L. Juwono


Many non-polar crystalline polymers do not dissolve, except at thetemperature near their crystalline melting points.Explanation:Crystallinity decreases as the melting point is approached andthe melting point is depressed by the presence of the solvent, thussolubility can often achieved at temperatures below melting point.

Examples:Linear PE (Tm = 135 °C), soluble in many liquids at 100 °C.PTFE (Tm = 325 °C), soluble in few liquids at >300 °C.Nylon-66 (Tm = 265 °C), soluble in liquids at RT.

For polymers, with the same chemical type and molecular weight,the branched species are more soluble than their linear species.

Theory of solubility thermodynamics of polymer solutions.

Ariadne L. Juwono


Solubility parameters

∆G = ∆H – T ∆Swhere: ∆G is the free energy of mixing (0).

For reasonably non-polar molecules and in the absence of hydrogen

bonding, ∆H is positive.

∆H = ν1 ν2 (δ1 – δ2)2

Where: ∆H is the heat of mixing/volume,ν1 ,ν2 are the fractions of solvent and polymer respectively,δ2 is the cohesive energy density or

the energy of vaporization/volume for small molecules orsolubility parameter.

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Table 7.1. Page 153 Billmeyer

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In the absence of strong interactions such as hydrogen bonding,

(δ1 – δ2) < 3.5 – 4.0.

The structure of a polymer determines δ2

where ρ is the density of polymer,E is the sum over the structural configuration of the repeating

unit in the polymer chain,M is the repeat molecular weight.

Solvents with high solubility have usually small and compact molecules,these kinetically good solvents do not need thermodynamically good.Solvents of a kinetically good and a thermodynamically good liquid areoften very powerful and rapid polymer solvents.

M

Eρδ2

∑=

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Table 7.2. Page 154 Billmeyer

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7.2. Conformations of dissolved polymer chains

Conformations are the arrangements of polymer chain in term ofrotations about single bonds.A polymer molecule is a randomly coiling mass most of whoseconformations occupy many times the volume of its segment.The average density of segments within a dissolved polymer molecule

is ≈ 10-4 – 10-5 g/cm3.

The polymer-solvent interaction forces determine the size of the molecular coil.A “good” solvent, where the polymer-solvent highly contact, the coilsare relatively extended.A “poor” solvent, where the polymer-solvent does not contact, thecoils are contracted.

The random-coil nature of the dissolved, molten, amorphous, and glassystates of high polymers is important.

Ariadne L. Juwono


The random coil arises from the relative freedom of rotation associatedwith the chain bonds of most polymers and the number of conformationsaccessible to the molecule.

Fig 7.2 Billmeyer

Example of a fully extended chain is all-trans planar zigzag carbon chain.

Some important terms:• Contour length,• Radius of gyration, : the root-mean-square distance between its ends,

• The root mean-square-root distance of the elements of the chain fromits centre of gravity,

( )1/22r

( )1/22s

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Freely jointed chainA simple model of a polymer chain consists of a series of x links oflength l joined in a linear sequence without restrictions on the anglesbetween successive bonds.

Classical random-flight method (Rayleigh, 1919)

( ) 1/21/2f2 lxr =

where f is the random-flight end-to-end distance,

is a characteristic property of the polymer chain structure and

independent of molecular weight.

M

r2

f

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Fig 7.3.

W is the probability to find such an array has a given end-to-end distance r.

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Short-range interactionsThe effect of short-range interactions on the dimensions of random-Coil polymers can be calculated from another model.

Modern polymer chemistry model (Flory, 1919)

Several effects are considered for this model.

•The restriction to fixed bond angle θ expands the chain by a factor of[(1 – cos θ)/(1 + cos θ)]1/2 or it is equal to √2 for C-C bonds.

•Restricted rotation steric hindrances, potential-energy barriers,resonance leading to rigid planar conformations increases dimensions.•Conformations by 2 atoms close together along chain further expansion•Pentane interference (interaction between 1st and 5th chain atoms ina sequence.

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The net results of all of these effects is called •A characteristic ratio of the square of the actual chain dimensions in the absence of longitudinal interactions or unperturbed dimensions

•The square of the random-flight end-to-end distance, l2x.

( )20r

Fig 7.3.

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Long-range interactions and the excluded volumeEach segment of a real chain exists within a volume from which all othersegments are excluded the excluded volume theory.

A statistical approachThe actual dimensions of the real chain:

where α is an expansion factor and depends on the nature of the solvent and the temperature.

α >>> “good” solvent and vice versa

When α = 1, the chain attains its unperturbed dimensions.At this condition, the temperature is called the Flory temperature, Θ.A solvent used at T = Θ is called a Θ solvent.

( ) ( )1/2201/22 rαr =

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7.3.Thermodynamics of polymer solutions

From the study of solution properties, it is possible to obtain informationabout the size and the shape of polymer molecules.

Simple liquid mixture

The free energy of dilution of a solution in an equilibrium between 2 phases

=

0

A

A

AP

Pln kT∆G

where ∆G is the free energy of dilution resulting from the transfer of one molecule of liquid A, from the pure liquid state with vapourpressure PA

0 to a large amount of solution with vapourpressure PA.

Colligative property of solution

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Ideal solution

Ideal solution is the simplest type of mixing between components A andB with the same size, shape, and force fields.

Raoult’s law: the partial vapour pressure of each component in the mixture is proportional to its mole fraction.

The pressure of liquid A: A0

A

BA

A0

AAnP

NN

NPP =

+=

where nA is the mole fraction of A.

AAnln kT∆G =

The total free energy of mixing:

)nln Nnln kT(N∆G

∆G N∆G N∆G

BBAA

BBAA

+=

+=

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In an ideal mixing, the heat of mixing, ∆H = 0.The entropy of mixing:

)nln Nnln k(N∆S BBAA +=

Types of mixing solutions:

• Ideal solutions, ∆H = 0.• Athermal solutions, ∆H = 0, ∆S ≠ ∆Sideal• Regular solutions, ∆S = ∆Sideal, H is finite.• Irregular solutions, both ∆H and ∆S deviate from the ideal values.

Many mixtures are regular solutions.Polymer solutions deviate from ideal solutions. Even the mole fractionis replaced with the volume fraction bad correlation withexperimental results.

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Entropy of mixing

Some assumptions are drawn for polymer solution:1. The polymer molecules consist of a large number x of chain segments

of equal length, flexibly joined together,2. Each link occupies 1 lattice site,3. The solution is concentrated so that the occupied lattice sites are

distributed randomly.

Flory-Huggins theory of polymer solutions:

)νln Nνln k(N∆S 2211 +=

21

1

1xNN

Nν

+=

21

2

2xNN

xNν

+=

where υ1 and υ2 are the volume fractions of the solvent and the polymer,respectively,x is the number of chain.

Ariadne L. Juwono


Heat and free energy of mixing

211 νkTNχ∆H =

)νNχνln Nνln kT(N∆G 2112211 ++=

Other thermodynamics quantities

The partial molar free energy of mixing:

where χ1is the interaction energy per solvent molecules / kT

)νχν x

11)ν -(1kT[ln G∆ 221221 +

−+=

The osmotic pressure:

+−+= ....)νχ2

1(

x

ν

V

kTπ 2

21

2

1

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The Flory-Huggins theories were compared with experimental dataof rubber in benzene. It is found that the partial molar heat ofdilution

was not observed.The entropy of mixing was in fair agreement with the theory.The other properties did not match with the theoretical values.

2

21kTνχ∆H =

)χ2

1(

VN

νA

1

10

2

2

2−≡

The coefficient of υ22 is known as the second virial coefficient A2

Ariadne L. Juwono


Dilute solutions

The dilute polymer solution is discontinuous in structure and consists ofdomains or clusters of polymer chain segments separated on the average by regions of polymer-free solvent.

The partial molar heat:

The partial molar entropy:

The partial molar free energy:

2

211 νkTκH∆ =

2

211 νkψS∆ =

2

2111 )νψ-kT(κG∆ =

2

1χψκ

111−=−

The Flory temperature:

1

1

ψ

TκΘ =

At T = Θ, the partial molar free energy due to polymer-solvent interactionsis zero and the deviations from ideal solution vanish.

Ariadne L. Juwono


7.4. Phase equilibrium in polymer solutions

Polymer-solvent miscibility

Equilibrium between amorphous polymer and solvent(s).

When the temperature of a polymer solution ↑ or ↓the solvent becomes thermodynamically poorer polymer and solvent are no longer miscible in all proportions

the mixture separates into 2 phases.

In this condition, χ1 exceeds a critical value (χ1 ≅ ½)

The phase separation takes place in 2 temperatures:• The upper critical solution temperature,• The lower critical solution temperature

2 critical values

of χ1

2 values of Θ

Ariadne L. Juwono


Binary polymer-solvent systems

In a binary system, the equilibrium between 2 phases occurs whenthe partial molar free energy for each component is equal in each phase.

(The 1st and 2nd derivatives of ∆G1 to ν2 = 0) see slide 20

The critical volume fraction:

The critical value of χ1:

The temperature at which phase separation begins:

1/21/22cX

1

x1

1ν ≈

+=

For a typical polymer, x ≅ 104, ν2c ≅ 0.01

1/2

21/2

1cx

1

2

1

2x

)x(1χ +≅

+=

+=

++=1/21/2

1cM

C1

Θ

1

2x

1

x

1

ψ

11

Θ

1

T

1

where C is a constant of the polymer-solvent system

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Ariadne L. Juwono


Multi component systems

This system consists of a heterogeneous polymer in a single solvent.

It is assumes that χ for all values of x are identical, only the size parameterx itself varies from one molecular species to another.

To make the calculation simple: σxν

νln

x

'

x =

where σ is a parameter that relates precipitated and dilute phases,νx’ and νx are the concentrations of species x in the precipitatedphase and the dilute phase, respectively.

So that: [ ]2'2

2

21'

n

'

2

n

2 )ν(1)ν(1χx

11ν

x

11νσ −−−+

−−

−=

where ν2’ and ν2 are the total polymer concentrations in 2 phases,xn is the number average of x.

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Region II: semidilute region

Θ

Θ)(Tτ

−=

Region I: dilute regionRegion III: semidilute &

concentrated Θ region

Region I’: Θ region

Region IV: negative

region of τ

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Polymer-polymer miscibility

The phase separation in polymer-polymer systems has been ininterest because the interesting properties of compatible polymerblends has been increased.In general, polymers mixed are totally immiscible.However, some of them existed.Some of the experimental data agree with the Flory-Huggins theory.

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7.5. Fractionation of polymers by solubility

Some techniques for fractionating polymers by solubility differencesare existed.

7.5.1. Bulk fractionation by nonsolvent solubility technique

This method takes place by adding nonsolvent to a dilute solutionof the polymer until a slight turbidity develops at the temperature offractionation homogeneous mixtureThe precipitation phase settles to a coherent layer and the supernatantphase is removed precipitated phase is added.This process is repeated until the polymer is isolated from theprecipitated phase (10% polymer).

The selection of solvent and precipitant are important. Some considerations are stability and volatility of the liquids and their ability to form a highly swollen, mobile gel phase.

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7.5.2. Column elution technique

The most important techniques & widely practiced for fractionating polymers are by solubility differences.

Solvent-gradient elutionPolymer is placed in contact with a series of liquids of gradually increasingsolvent power. Species of lowest molecular weight (the highest solubility)dissolve in the 1st liquid and higher molecular-weight fractions insubsequent liquid.To achieve a rapid equilibrium, the polymer is in a very thin film form.This process takes place in a mixing vessel, obtained a continuous gradient of solvent-nonsolvent composition and eluted through a column.

Thermal-gradient elutionA small temperature gradient is added from one to the other of the column.Each species experiences a series of solution and precipitation steps through temperature-gradient column.

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7.5.3. Analytical precipitation technique

Summative fractionationA series of polymer solutions is used. In each solution, part of thepolymer is precipitated and the point of fractionation being variedthroughout the series.

Turbidimetric titrationA precipitant is added slowly to a polymer solution. The turbidity dueto precipitated polymer is measured by the decrease in intensity ofa beam of transmitted light or by the increase in intensity of scatteredlight.

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7.5.4. Effect of polymer structure on solubility-based fractionation

Effect of chemical typeThe solubility of polymers is primarily determined by their chemicalcompositions. So that fractionation is likely to occur as a result ofthese compositions.

Effect of chain branchingBranching increases the solubility of high polymers. Branched polymersbeing separated will consist of a mixture of species, some with lowbranching and low molecular weight, others with more branched butwith higher molecular weight.

Effect of crystallinityFractionation by molecular weight can be done for precipitation of polymerto a crystalline phase, especially if crystalline melting point is a strong function of molecular weight.

chapter 7. polymer solutions 7.1. criteria for polymers solubility … · 2020. 3. 22. ·...

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